Fuel cell system and method for producing steam in a fuel cell system

Claim 2

A fuel cell system comprising: a fuel cell including a cathode section for receivinc oxidant process gas and an anode section for receiving fuel process gas; and means responsive to exhausted process gas and to gas at a higher temperature for producing steam.

Claim 3

A fuel cell system in accordance with claim 1 wherein: said steam producing means includes a heat exchanger for receiving exhausted process gas and said higher temperature gas in heat exchange relationship, whereby the temperature of said exhausted process gas is increased.

Claim 4

A fuel cell system in accordance with claim 2 wherein: said higher temperature gas is derived from gas of said system.

Claim 5

A fuel cell system in accordance with claim 3 wherein: the quantity of exhausted process gas received by said heat exchanger and the increased temperature of said received exhausted process gas are such as to enable production of said steam at a predetermined pressure.

Claim 6

A fuel cell system in accordance with claim 4 wherein: said fuel cell receives one of said oxidant and fuel process gases in excess of that required for electrochemical reaction for cooling of said cell; and the exhausted of said one of said oxidant and fuel process gases is the exhausted gas to which said steam producing means is responsive.

Claim 7

A fuel cell system in accordance with claim wherein: said exhausted process gas is exhausted oxidant process gas.

Claim 8

A fuel cell system in accordance with claim 6 further including: means for burning exhausted fuel process gas to produce said higher temperature gas.

Claim 9

A fuel cell system in accordance with claim 6 wherein: said fuel process gas is at a preselected pressure.

Claim 10

A fuel cell system in accordance with claim 8 further including: means for combining fresh supply fuel with said steam; and reforming means responsive to said combined fresh supply fuel and steam for.providing said fuel process gas through a reforming reaction.

Claim 11

A fuel cell system in accordance with claim 9 wherein: said predetermined pressure of said steam is such that said fuel process gas from said gas reforming means is at least at said preselected pressure.

Claim 12

A fuel cell system in accordance with claim l0 wherein: the quantity of exhausted process gas received by said heat exchanger and the increased temperature of said received exhausted process gas are such as to enable production of a predetermined quantity of steam at said predetermined pressure, said predetermined quantity being sufficient for said reforming reaction.

Claim 13

A fuel cell system in accordance with claim 10 wherein: said steam producing means further includes a steam generator for receiving water and said increased temperature process gas in heat exchange relationship to thereby generate said steam.

Claim 14

A fuel cell system in accordance with claim 9 wherein: said fuel process gas from said reforming means is at a first temperature higher than a preselected operating temperature for said cell; and said system-further includes means for reducing the temperature of said fuel process gas to a second temperature between said first temperature and.said preselected operating temperature; and a quantity of said second temperature fuel process gas forms said higher temperature gas.

Claim 15

A fuel cell system in accordance with claim 9 further including: means for burning a quantity of said fresh supply fuel to produce heating gas and for coupling said heating gas to said reformer for providing heat for said reforming reaction; means for combining a portion of said heating gas with a portion of exhausted oxidant process gas; and means for reducing the pressure of said combination of said heating gas and said portion of exhausted oxidant process gas, a quantity of said reduced pressure combination of gases forming said higher temperature gas.

Claim 16

A fuel cell system in accordance with claim 8 wherein: said preselected pressure is within the range of 30 to 200 psia.

Claim 17

'16. A fuel cell in accordance with claim 1, 2 or 3 wherein said fuel cell system further includes: a phosphoric acid electrolyte disposed between said anode and cathode sections.

Claim 20

A method in accordance with claim 17 wherein: said step of utilizing includes placing said quantities of exhausted process gas and higher temperature gas in heat exchange relationship, whereby the temperature of said quantity of exhausted process gas is increased.

Claim 21

A method in accordance with claim 18 wherein: said higher temperature gas is derived from a gas of said system.

Claim 22

A method in accordance with claim 19 wherein: the amount and temperature of said quantity of increased temperature exhausted process gas results in steam at a predetermined pressure.

Claim 23

A method in accordance with claim 20 wherein: said fuel cell receives one of said oxidant and fuel process gases in excess of that required for electrochemical reaction for cooling of said cell; and said step of obtaining is carried out by deriving a quantity of exhausted of said one of said oxidant and fuel process gases.

Claim 24

A method in accordance with claim 20 wherein: said exhausted process gas is exhausted oxidant process gas.

Claim 25

A method in accordance with claim 22 wherein: said method further includes burning exhuasted fuel process gas; and said step of utilizing is carried by employing a quantity of said burned exhausted fuel process gas as said higher temperature gas.

Claim 26

A method in accordance with claim 22 further comprising: combining a quantity of said steam with fresh supply fuel; and subjecting said combination of steam and fresh supply fuel to a reforming reaction to provide said fuel process gas.

Claim 27

A method in accordance with claim 24 wherein: said method further includes reducing the temperature - .of said fuel process gas produced by said reforming reaction; and said step of utilizing is carried out employing a quantity of said reduced temperature fuel process gas as said higher temperature-gas.

Claim 28

A method in accordance with claim 22 wherein: said method further includes: burning a quantity of fresh supply fuel to produce heated gas for use in said reforming reaction; combining a quantity of such heated gas with a portion of exhausted oxidant gas; and reducing the pressure of said combination of gases, a quantity of said reduced pressure combination of gases forming said higher temperature gas.